US573714A - Process of and apparatus for treating garbage - Google Patents
Process of and apparatus for treating garbage Download PDFInfo
- Publication number
- US573714A US573714A US573714DA US573714A US 573714 A US573714 A US 573714A US 573714D A US573714D A US 573714DA US 573714 A US573714 A US 573714A
- Authority
- US
- United States
- Prior art keywords
- vessel
- garbage
- naphtha
- pipe
- steam
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title description 16
- 239000004519 grease Substances 0.000 description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 20
- 239000012530 fluid Substances 0.000 description 16
- 230000000694 effects Effects 0.000 description 8
- 239000003795 chemical substances by application Substances 0.000 description 6
- 238000000605 extraction Methods 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 239000003153 chemical reaction reagent Substances 0.000 description 4
- 238000010276 construction Methods 0.000 description 4
- 238000003379 elimination reaction Methods 0.000 description 4
- 229920002456 HOTAIR Polymers 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 230000000295 complement Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000010981 drying operation Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000011068 load Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 241000894007 species Species 0.000 description 2
- 230000000576 supplementary Effects 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 239000006200 vaporizer Substances 0.000 description 2
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
Definitions
- My invention consists of a process and apparatus for the treatment, for the recovery of useful products therefrom, of wet garbage or other greasy material containinga large percentage of water, the process being in some respects allied to that set forth in Patent No. 466,57 9, granted to myself and C. F. Simonin on the 5th day of January, 1892.
- A represents a treating Vessel, which in the present instance is in the form of a cylinder having a detachable head A at one end and having in the top an opening a, provided with a cover-plate a, such opening being intended for the introduction of the garbage.
- the shape and construction of the treating vessel may, however, be varied to accord with the requirements in any particular case without departing from myinvention.
- the vessel has in the lower portion a steam-coil d, communicating through a valved pipe d with any available steamgenerator, which also communicates through a valved pipe f with a perforated coil f in the lower portion of the air, the temperature and dryness of which is v hot gaseous fluid may, if desired, be relied vessel.
- the said lower portion of the vessel also communicates through a valved pipe 9 with a naphtha tank or vaporizer and through another valved pipe, 7L, with a superheater of any desired character.
- the superheater may consist of a pipe-coil located in the breechin g or discharge-flue of the steam-generator; or, if air is employed as the heating agent, said pipe It may communicate with any available form of air-heater, or it may receive the products of combustion direct from a suitable furnace.
- the lower portion of the treating vessel communicates through a valved pipe m, havin g a valved branch m, with any desired form of still or settler, and the upper portion of the vessel communicates through a valved piped with a condenser of appropriate construction.
- the process of treating the garbage is as follows: Into the empty vessel, closed at one end and having the cover-plate ct removed, is run a truck B, having the lowermost of its series of trays thereon, the truck being stopped beneath the opening a, so that the garbage may be introduced through said opening until the tray D upon the truck has been filled; Another tray isthen placed on top of the first, and after the same has been filled a third tray is placed thereon, and so on until the entire complement of trays carried by said truck has been properly filled, whereupon the truck with its loaded trays is pushed along to the end of the vessel and a second truck is run in beneath the opening a, and when this second truck has received its load of filled trays it is likewise pushed along into the vessel, so as to make room for a third truck, the operations being repeated until the vessel is filled.
- the front head A and cover-plate a are then secured in place and the naphtha or naphtha-vapor is-permitted to enter the vessel through the valved pipe g, the valves in the pipes d, f, h, on, and m being closed.
- the valve in the pipe 9 is closed and the naphthamay be heated or kept hot by the steam-coilcl, the valve in the piped being opened, and after the treatment has continued for a proper length of time the valve in the pipe m may be opened, so as todraw off the water which has accumulated in the vessel, the valve in said pipe m being then closed and the naphtha, carrying with it the grease in solution, permitted to escape to the still or settler through the pipe on.
- the treating vessel may be vertical instead of horizontal, the trays D in this case being lowered one after another into the vessel and lifted in succession from the vessel after-the completion of the treatment.
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
Description
(No lodel.)
vI. M. SIMONIN.
PROCESS or AND APPARATUS FOR TREATING GARBAGE. No. 573,714. Patented Dec. 22, 1896.
n I u l I n I I I I n I I u I u n I I I I II FIG. 2.
v a l? m; J J
j I I a 1 a ft a Znve ni-o-r; W2 $72858 es f5 Sac M Simon-11w Ynzuonms PETERS :04 wafouwo, WASHINGTON 0 cv UNITED STATES PATENT OFFICE.
ISAAC M. SIMONIN, OF PHILADELPHIA, PENNSYLVANIA.
PROCESS OF AND APPARATUS FOR TREATING GARBAGE.
SPECIFICATION forming part of Letters Patent No. 573,714, dated December 22, 1896.
Application filed August 18, 1894. Serial No. 520,659. (No model.)
To all whom it may concern:
Be it known that I, ISAAC M. SIMONIN, a citizen of the United States, residing in Philadelphia, Pennsylvania, have invented certain Improvements in the Treatment of Garbage and in Apparatus Employed in Connection Therewith, of which the following is a speci fication.
My invention consists of a process and apparatus for the treatment, for the recovery of useful products therefrom, of wet garbage or other greasy material containinga large percentage of water, the process being in some respects allied to that set forth in Patent No. 466,57 9, granted to myself and C. F. Simonin on the 5th day of January, 1892.
The object of my present invention is mainly to expedite the treatment of the garbage and thereby render the process more economical than that forming the subject of said patent. This object I attain in the manner hereinafter set forth, reference being had to the accompanying drawings, in which Figure 1 is a transverse section of apparatus which may be employed in carrying out my invention, and Fig. 2 is a longitudinal section of the same.
In carrying out the process forming the subject of the patent before referred to the garbage was deposited in a single mass in a treating vessel and there subjected to the action of a heated liquid reagent, such as naphtha, which has a less specific gravity than water, the function of this liquid reagent being twofold: first, to dissolve the grease and fat contained in the garbage, and, secondly, to displace the water in the mass, so that the latter would collect in the bottom of the vessel and could be drawn off therefrom, the naphtha, with the grease in solution therein, being carried to a still, where the separation of the naphtha from the grease was effected, provision being also made for heating the naphtha in the treating vessel, so as to facilitate its action in dissolving the grease, and further provision being made for the introduction of steam into the treating vessel after the withdrawal of the liquid naphtha and grease, so as to vaporize the naphtha still remaining in the mass of garbage. It has been found in practice that in carrying out this process the garbage must be treated a nu1nber of times in succession in order to effect the thorough elimination of the water therefrom for the purpose of reducing the mass remaining in the vessel to the desired dry and inodorous condition.
With the view of materially lessening the time of treatment I now subdivide the mass of garbage so that the agent employed in the treatment of the same can readily gain ac cess to all parts of the mass, and I effect the elimination of all or almost all of the water from the mass by the use of a dry hot gas eous fluid, such as superheated steam or hot materially in excess of that of the steam used for driving off the naphtha from the garbage, the effect of the action of this dry hot gaseous fluid being to vaporize the water contained in the garbage, the vapor escaping from the treating vessel and being conveyed to the condenser. This treatment with a dry upon to effect the melting of the fat or grease in the garbage, but it is by preference supplementary to the treatment of the garbage with heated naphtha, as above described.
In the drawings, A represents a treating Vessel, which in the present instance is in the form of a cylinder having a detachable head A at one end and having in the top an opening a, provided with a cover-plate a, such opening being intended for the introduction of the garbage. The shape and construction of the treating vessel may, however, be varied to accord with the requirements in any particular case without departing from myinvention.
To suitable rails b within the treating vessel are adapted the wheels of trucks B, each of which carries a series of shallow pans or trays D, preferably perforated in the bottom, these trays being of a width limited by the diameter of the vessel and of such length that their size and weight will not preclude the ready handling of the same. The vessel has in the lower portion a steam-coil d, communicating through a valved pipe d with any available steamgenerator, which also communicates through a valved pipe f with a perforated coil f in the lower portion of the air, the temperature and dryness of which is v hot gaseous fluid may, if desired, be relied vessel. The said lower portion of the vessel also communicates through a valved pipe 9 with a naphtha tank or vaporizer and through another valved pipe, 7L, with a superheater of any desired character. Thus, if steam is the heating agent employed, the superheater may consist of a pipe-coil located in the breechin g or discharge-flue of the steam-generator; or, if air is employed as the heating agent, said pipe It may communicate with any available form of air-heater, or it may receive the products of combustion direct from a suitable furnace.
The lower portion of the treating vessel communicates through a valved pipe m, havin g a valved branch m, with any desired form of still or settler, and the upper portion of the vessel communicates through a valved piped with a condenser of appropriate construction.
The process of treating the garbage is as follows: Into the empty vessel, closed at one end and having the cover-plate ct removed, is run a truck B, having the lowermost of its series of trays thereon, the truck being stopped beneath the opening a, so that the garbage may be introduced through said opening until the tray D upon the truck has been filled; Another tray isthen placed on top of the first, and after the same has been filled a third tray is placed thereon, and so on until the entire complement of trays carried by said truck has been properly filled, whereupon the truck with its loaded trays is pushed along to the end of the vessel and a second truck is run in beneath the opening a, and when this second truck has received its load of filled trays it is likewise pushed along into the vessel, so as to make room for a third truck, the operations being repeated until the vessel is filled. The front head A and cover-plate a are then secured in place and the naphtha or naphtha-vapor is-permitted to enter the vessel through the valved pipe g, the valves in the pipes d, f, h, on, and m being closed. hen the proper amount of naphtha has entered the vessel, the valve in the pipe 9 is closed and the naphthamay be heated or kept hot by the steam-coilcl, the valve in the piped being opened, and after the treatment has continued for a proper length of time the valve in the pipe m may be opened, so as todraw off the water which has accumulated in the vessel, the valve in said pipe m being then closed and the naphtha, carrying with it the grease in solution, permitted to escape to the still or settler through the pipe on. After the naphtha, with the grease in solution therein, has been discharged from the vessel communication between the latter and the still or settler is cut off and the valve in the V pipe h is opened, so that the superheated steam, air, or other dry hot gaseous fluid is admitted to the vessel. This fluid so acts upon' the masses of garbage as to vaporize the water or most of the water therein eonis necessary in order to eifect the desired result, that is to say, the complete extraction of the grease or fat from the garbage, steam being finally admitted from the coil f in order to vaporize and carry off through the pipe 01 the naphtha remaining in the garbage. For this purpose the direct action of steam is necessary, so that the naphtha can subsequently be recovered by condensation-hence the provision of the pipe f in addition to the superheated steam or hot-air pipe h. The cover-platesn' and A are finally removed and the trays taken out,emptied, reinserted, and refilled prior to a repetition of the operation.
By the use of the dry hot gaseous fluid for efiecting the vaporization of the water in the garbage a much less number of treatments of each charge is necessary than if the naphtha or other extraction process alone is used. Hence the operation is facilitated and the capacity of the plant very materially increased.
It will be observed that the entire treatment of the garbage is eifected in one and the same apparatus Without rehandling, so that the process is much more economical than those which involve the rcmovalof the garbage from the extracting or digesting vessel after the extraction of the grease, in order that it maybe subsequently deprivedof its moisture by submitting it to a drying operation.
In some cases the treating vessel may be vertical instead of horizontal, the trays D in this case being lowered one after another into the vessel and lifted in succession from the vessel after-the completion of the treatment.
Having thus described'my invention, I claim and desire to secure by LettersPatent- 1. The mode herein described of treating grease or fat, and finally to the direct action of live steam whereby the solvent remaining in the massWill be vaporized and driven off, to be recovered-from the steam by condensation, substantially as specified.
2. In apparatus for treating garbage, the comblnation of a vessel, means for closing the same,trucks adapted to be run into said will vessel, and each having a series of trays In testimony whereof I have signed my mounted one above another, outlets for liqname to this specification in the presence of uid and vapor from said Vessel, an inlet for two witnesses.
grease-extractin g fluid, another inlet for awa- ISAAC M. SIMONIN. ter-vaporizing fluid, a closed steam-coil and a YVitnesses: steam-discharge pipe within the vessel, sub- XVILLIAH A. BARR,
stztntially as specified. JOSEPH H. KLEIN. B
Publications (1)
Publication Number | Publication Date |
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US573714A true US573714A (en) | 1896-12-22 |
Family
ID=2642410
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US573714D Expired - Lifetime US573714A (en) | Process of and apparatus for treating garbage |
Country Status (1)
Country | Link |
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US (1) | US573714A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2788275A (en) * | 1950-01-26 | 1957-04-09 | Wacker Chemie Gmbh | Process for making fat-free animal feed products |
-
0
- US US573714D patent/US573714A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2788275A (en) * | 1950-01-26 | 1957-04-09 | Wacker Chemie Gmbh | Process for making fat-free animal feed products |
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